EP0569150B1 - Polyester laminates - Google Patents

Polyester laminates Download PDF

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Publication number
EP0569150B1
EP0569150B1 EP93302979A EP93302979A EP0569150B1 EP 0569150 B1 EP0569150 B1 EP 0569150B1 EP 93302979 A EP93302979 A EP 93302979A EP 93302979 A EP93302979 A EP 93302979A EP 0569150 B1 EP0569150 B1 EP 0569150B1
Authority
EP
European Patent Office
Prior art keywords
polyester
acid
paper
laminates
aliphatic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP93302979A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP0569150A2 (en
EP0569150A3 (index.php
Inventor
Yoshihiro c/o Showa Denko K.K. Moteki
Nobutaka c/o Showa Denko K.K. Fujiwara
Yukiharu c/o Showa Denko K.K. Furuichi
Eiichiro Takiyama
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
Showa Highpolymer Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from JP4117656A external-priority patent/JP2709236B2/ja
Priority claimed from JP11765792A external-priority patent/JP3153621B2/ja
Priority claimed from JP4117653A external-priority patent/JP2851478B2/ja
Priority claimed from JP4117654A external-priority patent/JP2709234B2/ja
Priority claimed from JP4117655A external-priority patent/JP2709235B2/ja
Priority claimed from JP11919792A external-priority patent/JP3238466B2/ja
Priority claimed from JP4120782A external-priority patent/JP2589908B2/ja
Application filed by Showa Denko KK, Showa Highpolymer Co Ltd filed Critical Showa Denko KK
Publication of EP0569150A2 publication Critical patent/EP0569150A2/en
Publication of EP0569150A3 publication Critical patent/EP0569150A3/xx
Publication of EP0569150B1 publication Critical patent/EP0569150B1/en
Application granted granted Critical
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/16—Making expandable particles
    • C08J9/18—Making expandable particles by impregnating polymer particles with the blowing agent
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/10—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of paper or cardboard
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/36—Layered products comprising a layer of synthetic resin comprising polyesters
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08—Processes
    • C08G18/0895—Manufacture of polymers by continuous processes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40—High-molecular-weight compounds
    • C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
    • C08G18/4236—Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40—High-molecular-weight compounds
    • C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
    • C08G18/4236—Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups
    • C08G18/4238—Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups derived from dicarboxylic acids and dialcohols
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40—High-molecular-weight compounds
    • C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
    • C08G18/4236—Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups
    • C08G18/4238—Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups derived from dicarboxylic acids and dialcohols
    • C08G18/4241—Polycondensates having carboxylic or carbonic ester groups in the main chain containing only aliphatic groups derived from dicarboxylic acids and dialcohols from dicarboxylic acids and dialcohols in combination with polycarboxylic acids and/or polyhydroxy compounds which are at least trifunctional
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40—High-molecular-weight compounds
    • C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
    • C08G18/4266—Polycondensates having carboxylic or carbonic ester groups in the main chain prepared from hydroxycarboxylic acids and/or lactones
    • C08G18/4283—Hydroxycarboxylic acid or ester
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40—High-molecular-weight compounds
    • C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
    • C08G18/4266—Polycondensates having carboxylic or carbonic ester groups in the main chain prepared from hydroxycarboxylic acids and/or lactones
    • C08G18/4286—Polycondensates having carboxylic or carbonic ester groups in the main chain prepared from hydroxycarboxylic acids and/or lactones prepared from a combination of hydroxycarboxylic acids and/or lactones with polycarboxylic acids or ester forming derivatives thereof and polyhydroxy compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40—High-molecular-weight compounds
    • C08G18/48—Polyethers
    • C08G18/4854—Polyethers containing oxyalkylene groups having four carbon atoms in the alkylene group
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/16—Dicarboxylic acids and dihydroxy compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/16—Dicarboxylic acids and dihydroxy compounds
    • C08G63/20—Polyesters having been prepared in the presence of compounds having one reactive group or more than two reactive groups
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/91—Polymers modified by chemical after-treatment
    • C08G63/914—Polymers modified by chemical after-treatment derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/916—Dicarboxylic acids and dihydroxy compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18—Manufacture of films or sheets
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/12—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
    • C08J9/14—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent organic
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00—Formation of filaments, threads, or the like
    • D01D5/42—Formation of filaments, threads, or the like by cutting films into narrow ribbons or filaments or by fibrillation of films or filaments
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/62—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters
    • D01F6/625—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters derived from hydroxy-carboxylic acids, e.g. lactones
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/70—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyurethanes
    • D—TEXTILES; PAPER
    • D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H13/00—Other non-woven fabrics
    • D04H13/02—Production of non-woven fabrics by partial defibrillation of oriented thermoplastics films
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2003/00—Use of starch or derivatives as moulding material
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2101/00—Manufacture of cellular products
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2110/00—Foam properties
    • C08G2110/0008—Foam properties flexible
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2230/00—Compositions for preparing biodegradable polymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2250/00—Compositions for preparing crystalline polymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2201/00—Foams characterised by the foaming process
    • C08J2201/02—Foams characterised by the foaming process characterised by mechanical pre- or post-treatments
    • C08J2201/03—Extrusion of the foamable blend
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2367/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
    • C08J2375/04—Polyurethanes
    • C08J2375/06—Polyurethanes from polyesters

Definitions

  • the present invention relates to polyester laminates formed by melt-extruding an aliphatic polyester onto a base selected from paper or cloth, for example, release base materials, base material for paper containers having excellent heat stability and mechanical strength which are prepared by using aliphatic polyesters with biodegradability and sufficiently high molecular weights and specific melt properties for practical use.
  • a release base material one comprising a release layer laminated on a filling layer on one or both sides of a paper or a cloth has been well known, wherein said filling layer is a low density polyethylene having a long branched chain obtained by the ordinary high-pressure method, a medium density polyethylene obtained by blending a low density polyethylene with a high density polyethylene, or a composition obtained by blending a low density polyethylene with polypropylene.
  • paper cups such as used for foods and drinks, for example, coffee, soup, miso-soup and instant noodles
  • paper trays for food for example, pizza, daily dishes and food for microwave ovens and the like
  • a resin composition as same as afore-mentioned is conventionally laminated to provide a water-repellent layer.
  • the base material for paper containers used for hot drinks and foods such as paper cups or paper trays
  • EP-A-0 323 700 and EP-A-0 448 294 disclose polyesters for use as stiffening materials. According to EP-A-0 323 700, by selection of the molecular weight of the polyester chains in the range 1,200-10,000 and the proportion of isocyanate, it is possible to control the time during which the material is suitable for shoemaking operations.
  • polyester material according to EP-A-0 448 294 is blended with a filler in the absence of harmful isocyanate.
  • the object of the present invention is to develop a release base material filled with a polymer which can be molded at a low temperature in order to minimize the volume of generated smoke in the melt-coating process, which has good bonding and firm-adhesive properties to the base material which is paper or cloth and which can be decomposed by natural and ordinary microorganisms in the earth.
  • the another object of the present invention is to develop a novel base material for a paper-made container, by which the problems concerning the odor of the oxidatively deteriorated polyolefin remaining on the paper-made container because of the high temperature lamination and the generation of a great volume of smoke can be solved, and which gives the paper-made container biodegradability and is advantageous to the preservation of the natural environment, where undecomposable materials of the used container have been accumulated.
  • the above-mentioned object has been achieved by the development of aliphatic polyester laminates formed by melt-extruding onto a base selected from paper or cloth an aliphatic polyester containing 0.03 - 3.0% by weight of urethane bonds and having a number average molecular weight Mn of more than 10,000, the aliphatic polyester having a melt viscosity of 1.0 x 10 3 - 1.0 x 10 5 poises at a temperature of 190°C and a shear rate of 100 sec -1 , and having a melting point of 70 - 200°C.
  • the aliphatic polyester of the present invention mainly consists of a polyester obtained by reacting two components of glycols and dicarboxylic acid (or acid anhydrides thereof), and if necessary as a third component, with at least one polyfunctional component selected from the group consisting of trifunctional or tetrafunctional polyols, oxycarboxylic acids, and polybasic carboxylic acids (or acid anhydrides thereof).
  • the aliphatic polyesters are prepared by reacting relatively high molecular weight polyester prepolymers which have hydroxyl groups at both ends with diisocyanate so as to make them even higher molecular weight polymer.
  • the polyester prepolymers used in these polyurethane foams, coatings and adhesives are prepolymers having a low molecular weight and a number-average molecular weight of 2,000-2,500 which is the maximum that can be prepared by non-catalytic reaction.
  • the content of diisocyanate should be as much as 10-20 parts by weight in relation to 100 parts by weight of this low molecular weight prepolymer.
  • polyesters which are obtained by reacting a large amount of diisocyanate with a low molecular weight polyester prepolymers as a raw material cannot be used as the plastic raw material for the base materials of the present invention.
  • the polyester prepolymers to obtain the aliphatic polyesters used in the present invention are relatively high molecular weight saturated aliphatic polyesters having substantially hydroxyl groups at the ends thereof, number-average molecular weights of more than 10,000, and melting point of 60°C or higher, which are obtained by reacting glycols and dibasic carboxylic acids (or acid anhydrides thereof) in the presence of catalysts.
  • polyester prepolymers having a number-average molecular weight of lower than 5,000 When a prepolymer having a number-average molecular weight of lower than 5,000 is used, the small amounts of 0.1-5 parts by weight of diisocyanate used in the present invention cannot provide polyesters for extrusion coating having good physical properties.
  • polyester prepolymers having number-average molecular weights of 5,000 or higher are used, with hydroxyl values of 30 or less, the use of small amounts of diisocyanate even under severe conditions such as a molten state and the like can produce high molecular weight polyesters without gelation as the reaction is not affected by remaining catalyst.
  • the polymer for the base materials of the present invention has a repeated chain structure in which a polyester prepolymer having a number-average molecular weight of more than 10,000 and consisting of an aliphatic glycol and aliphatic dicarboxylic acid is combined through the urethane bonds derived from diisocyanate as a coupling agent.
  • a release base material which essentially comprises an aliphatic polyester having a melt viscosity of 1.0 x 10 3 - 1.0 x 10 5 poises at a temperature of 190°C and a shear rate of 100 sec -1 and having a melting point of 70 - 200°C as a filling layer of, for example, adhesive sheets, binding tapes and the like.
  • melt-coating is proceeded at a low temperature, very little smoke, which has been a cause of community problems, is generated if at all, and concomitant problems such as worsening of the working environment and environmental pollution around the factory by exhausted smoke, can be solved.
  • the resin used in the present invention is biodegradable by microorganisms, they can be disposed of by waste disposal means using buried in the earth.
  • glycols which can be used as a reaction component include aliphatic glycols. Among them those having a straight chain alkylene group with even number carbon atoms of 2, 4, 6, 8 and 10 such as: ethylene glycol, 1,4-butanediol, 1,6-hexanediol, 1,8-octanediol, 1,10-decanediol, and mixtures thereof are preferable.
  • glycols those having a smaller number of carbon atoms, such as ethylene glycol, 1,4-butanediol and 1,6-hexanediol, are preferable because they can produce an aliphatic polyester having a high crystalinity and a high melting point.
  • ethylene glycol and 1,4-butanediol are most suitable because they produce good results.
  • succinic acid, succinic anhydride and an acid mixture of succinic acid or succinic anhydride and another dicarboxylic acid such as adipic acid, suberic acid, sebacic acid or 1,10-decanedicarboxylic acid are preferable.
  • the mixing ratio of succinic acid is at least 70 mol%, preferably at least 90 mol%, and the mixing ratio of the other carboxylic acids is 30 mol% or less, preferably 10 mol% or less.
  • a combination of 1,4-butanediol and succinic acid or succinic anhydride and a combination of ethylene glycol and succinic acid or succinic anhydride are particularly preferable for the present invention because the combinations exhibit melting points close to that of polyethylene.
  • glycols and dicarboxylic acid may be added as a third component at least one polyfunctional component selected from the group consisting of trifunctional or tetrafunctional polyols, oxycarboxylic acid, and polybasic carboxylic acids (or acid anhydrides thereof).
  • This third component which causes the branching of long chains, can impart desirable properties in molten state to the polyester prepolymer, because the ratio of weight-average molecular weight (MW)/ number-average molecular weight (Mn), i.e., the molecular weight distribution, increases with increases in its molecular weight.
  • a trifunctional component of 0.1-5 mole %, or a tetrafunctional component of 0.1-3 mole % is added relative to 100 mole % of the total of aliphatic dicarboxylic acid (or acid anhydride thereof) components.
  • polyfunctional components as the third component include trifunctional or tetrafunctional polyols, oxycarboxylic acids, and polybasic-carboxylic acids.
  • the trifunctional polyols representatively include trimethylol propane, glycerin or anhydrides thereof.
  • the tetrafunctional polyols representatively include pentaerythritol.
  • the trifunctional oxycarboxylic acid components are divided into the two types of (i) a component which has two carboxyl groups and one hydroxyl group in one molecule, and (ii) another component which has one carboxyl group and two hydroxyl groups in one molecule.
  • Malic acid which has two carboxyl groups and one hydroxyl group in one molecule becomes practical and sufficient to the purposes of the present invention in view of commercial availability at low cost.
  • the tetrafunctional oxycarboxylic acid components are the following three types of components:
  • trimesic acid propane tricarboxylic acid and the like
  • trimesic anhydride is practical for the purposes of the present invention.
  • tetrafunctional polybasic carboxylic acid or anhydride thereof
  • pyromellitic anhydride, benzophenone tetracarboxylic anhydride and cyclopentane tetracarboxylic anhydride are practical and sufficient to the purposes of the present invention.
  • glycols and dibasic acids are mainly consisted of aliphatic series, while small amounts of other components, for example, aromatic series may be concomitantly used.
  • aromatic series may be concomitantly used.
  • These other components may be blended and copolymerized in amounts up to 20% by weight, preferably up to 10% by weight, and more preferably up to 5% by weight because using these compounds degrades biodegradability.
  • the polyester prepolymer for aliphatic polyesters to be used in the present invention has hydroxyl groups at the terminals. To introduce the hydroxyl groups, it is necessary that glycols are used somewhat excessively.
  • Examples of the deglycol-reaction catalysts include titanium compounds such as acetoacetoyl type titanium chelate compounds and organic alkoxy titanium compounds and the like. These titanium compounds can be used in combination. Examples of compounds used in combination include diacetoacetoxy oxytitanium (Nippon Chemical Industry Co., Ltd.; Nursem Titanium) tetraethoxy titanium, tetrapropoxy titanium, tetrabutoxy titanium and the like. The amount of the titanium compound used is 0.001-1 part by weight, and preferably 0.01-0.1 part by weight relative to 100 parts by weight of the polyester prepolymer. These titanium compounds may be blended before the esterification, or may be blended immediately before the deglycol-reaction.
  • titanium compounds such as acetoacetoyl type titanium chelate compounds and organic alkoxy titanium compounds and the like. These titanium compounds can be used in combination. Examples of compounds used in combination include diacetoacetoxy oxytitanium (Nippon Chemical Industry Co., Ltd.; Nursem
  • polyester prepolymers having an acid-average molecular weight of more than 10,000, and preferably at least 20,000 and a melting point of 60°C or higher, can be generally obtained easily. It is even more preferable if these polyester prepolymers have crystallization.
  • polyester prepolymer which has a number-average molecular weight of more than 10,000, and whose terminal groups are substantially hydroxyl groups is added diisocyanate in order to increase its number-average molecular weight.
  • diisocyanate examples include 2,4-tolylene diisocyanate, a mixture of 2,4-tolylene diisocyanate and 2,6-tolylene diisocyanate, diphenylmethane diisocyanate, 1,5-naphthylene diisocyanate, xylylene diisocyanate, hydrogenated xylylene diisocyanate, hexamethylene diisocyanate, isophorone diisocyanate and the like.
  • hexamethylene diisocyanate is preferably used in terms of hue of prepared resins, reactivity at the time of blending polyesters, and the like.
  • the adding amounts of the diisocyanate is 0.1 - 5 parts by weight, and preferably 0.5-3 parts by weight relative to 100 parts by weight of polyester prepolymer.
  • the addition is preferably performed when the polyester is in a uniformly melted state under easily stirrable conditions.
  • the diisocyanate it is not impossible for the diisocyanate to be added to the polyester prepolymer in the form of a solid and melted and mixed through an extruder, adding the agents in a polyester preparation unit, or adding them to polyester prepolymer in a melt state (for example, in a kneader) is more practical.
  • the amount of urethane bonds is 0.03 - 3.0% by weight, preferably 0.05-2.0% by weight, and more preferably 0.1 - 1.0% by weight.
  • the amount of urethane bonds is measured by 13 C NMR, showing good correlation with tne charged amount.
  • the aliphatic polyester to be used in the present invention is required to have selected melt properties for base materials. That is, in release base materials or base materials for paper containers, the aliphatic polyester resin to be used in the present invention has a melt viscosity of 1.0 x 10 3 - 1.0 x 10 5 poises at 190°C at a shear rate of 100 sec -1 . Those having a melt viscosity of lower than 1.0 x 10 3 poises have defects in that surging and non-uniformity of the resin temperature easily occur and extruding stability is lost in the extrusion moulding process.
  • melt viscosity is preferably within the range of 2.0 x 10 3 - 2.0 x 10 4 poise, and more preferably 2.5 x 10 3 - 1.2 x 10 4 poise.
  • the melting point of the aliphatic polyester to be used in the present invention is 70°C - 200°C.
  • a melting point of lower than 70°C gives poor heat resistance in the silicone coating process and in the adhesive agent coating process.
  • Such an aliphatic polyester must be treated at low temperature, and requires a long time to dry and remove the solvents of silicone or adhesive agent. Accordingly, an aliphatic polyester having such a melting point is excluded.
  • the melting point of the aliphatic polyester is preferably 60°C - 150°C, and more preferably 80°C - 130°C .
  • the melt temperature of the aliphatic polyester to be used for the base material for paper container in the present invention is preferably 85°C -200°C .
  • a melting point of lower than 85°C is not preferable, since it will give paper cups and trays poor heat resistance to hot drinks, etc. resulting in release and melting of the laminated aliphatic polyester composition and release of the joint.
  • a melting point higher than 200°C of melting point is also not preferable, since it makes the biodegradation rate of the paper cups or trays slow down when decomposed by microorganisms in the earth. Therefore, the melt temperature is preferably 90°C -150°C , and more preferably 100°C -140°C .
  • the base material for a paper-made container can be prepared by laminating the aliphatic polyester resin obtained by the above-mentioned process on a base paper by T-die method.
  • the temperature of the resin to be extruded is 150-290°C .
  • the melt viscosity is too high, and hence the motor load becomes large and the productivity decreases in the extrusion-molding process, and it becomes difficult to make a thin melt film in the lamination-molding process as well.
  • the resin temperature is higher than 290°C
  • the resin composition deteriorates and loses extrusion stability because of the occurrence of surging, and it is difficult to lamination-mold since the neck-in [a phenomenon in which during the lamination-molding process the width of the melt film discharged from T-die becomes narrow in the space between the melt film and a base material, where the melt film has not yet contacted with the base material, and it is expressed by the difference of widths between the melt film at the T-die outlet and the laminated film laminated on the base material] of the melt film is large and not stable in the lamination-molding process.
  • the resin temperature is preferably 160-285°C , and more preferably 170-275°C.
  • a general screw-type extruder and laminator can be used in the process for making a base material for paper container of the present invention.
  • An example of a molding process is one in which a melt resin comprising an aliphatic polyester resin is extruded on one side of the base paper supplied at a speed of 20 - 200 m/min, and seal-joined by press with the base paper at the position between the cooling roll and the press roll. After cooling and hardening the melt resin by contact with the surface of the cooling roll, this is rolled up or piled up on the cutting stand through the continuous cutter.
  • the cooling roll to be used in the present invention may be any one used for surface-finishing such as a mat finishing type, semi-mat finishing type, mirror finishing type and the like.
  • a mat finishing type of cooling roll is preferable in view of the stacking property of the resulting paper cups and trays (that is, paper cups, etc. are pulled out one by one from their stacks, that is required when used for vending machines) and releasability of resultants from the roll in the lamination-molding process.
  • the surface of the melt film to be contacted with the plate paper may be sprayed with ozone gas and the like in order to strengthen the firm-adhesiveness and bonding property to the board paper.
  • adhesive-applying agents such as terpene-based resins and adhesive resins such as ionomers, ethylene-acrylate ester copolymer and acid-modified polyolefines may be added to the aliphatic polyester composition so that the functions of the laminated paper of the present invention would not be lost.
  • the method in which the board paper is previously treated by, for example, anchor-coat treatment, corona treatment, flame treatment, and the like may be employed in order to strengthen the firm-adhesiveness and the bonding property to the laminated film.
  • an alphatic polyester prepared by using additionally a small amount (0.2 - 1.0 mol %) of polyols which has more than 3 of hydroxyl group (-OH) or polybasic carboxylic acid monomer which has more than 3 of carboxyl group (-COOH) in one molecule, has a widened molecular weight distribution and long chain branches, as molding pressure becomes lower resulting in smaller necking-in and surging, thus improving film formability.
  • the polyester having no long chain branch alone can be naturally employed, alternatively, a polyester which have long chain branch may be used, or mixture thereof may also be used. However, when smaller necking-in is desired, a polyester having long chain branch may preferably be blended.
  • lubricants such as VITON, are especially very effective in improving the smoothness of the surface.
  • a 700 L reactor was purged with nitrogen, then 183 kg of 1,4-butanediol and 224 kg of succinic acid were charged in it. After the temperature was elevated under nitrogen stream, esterification by dehydration condensation was carried out for 3.0 hr at 195-210°C , and after ceasing nitrogen charge, for further 3.5 hr under reduced pressures of 15-5 mmHg.
  • a sample collected had an acid value of 6.3 mg/g, a number-average molecular weight (Mn) of 5,200 and a weight average molecular weight (Mw) of 10,100. Subsequently, 34 g of tetraisopropoxy titanium, a catalyst, was added at normal pressures under nitrogen stream.
  • the temperature was elevated to carry out a deglycol-reaction at temperatures of 215-220°C under reduced pressures of 5-0.2 mmHg for 7.5 hr.
  • a sample collected had a number-average molecular weight (Mn) of 18,600 and a weight average molecular weight (Mw) of 50,300.
  • the yield of resulting polyester prepolymer (A1) was 339 kg except condensate water.
  • the obtained polyester (B1) was a slightly ivorylike white, waxy crystal, and had a melting point of 110°C , a number-average molecular weight (Mn) of 29,500 a weight-average molecular weight (Mw) of 127,000, a MFR (190°C) of 9.2 g/10 min, a viscosity of 170 poises in a 10% ortho-chlorophenol solution and a melt viscosity of 8.0 ⁇ 10 3 poises at a temperature of 190°C at a shear rate of 100 sec -1 .
  • the average molecular weight was measured by a Shodex GPC System-11 (Showa Denko, gel permiation chromatography) using a HFIPA solution containing 5 mmol CF 3 COONa (concentration of 0.1% by weight) as a medium.
  • a calibration curve was drawn using a PMMA standard sample (Shodex Standard M-75, Showa Denko).
  • the selvage of the thin film was stable and there was little generation of smoke in the molding process. In this manner, the release base material could be stably molded.
  • the obtained release base material had sufficient close-adhesiveness between paper and polyester, and cohesive failure of the paper was observed in the peeling test with no interfacial peeling.
  • the release base material was cut into a 10 cm ⁇ 20 cm of rectangular pieces and they were mounted on square frames made of stainless steel with the pieces held between polyethylene nets. The obtained test pieces were then buried in the earth at a depth of 10 cm to evaluate biodegradability.
  • the test site was the grounds of Kawasaki Plastics Laboratory, SHOWA DENKO K.K. (Kawasaki-ku, Kawasaki-shi). After three months, the test pieces were dug up from the earth. The polyester thin films were more decomposed than paper fibers and had crumbled into decay.
  • the polyester (B1) was molded by using the same laminator as Example 1, under the same conditions as Example 1 except for employing a molding temperature of 190°C and a line speed of 100 m/min. In this molding process, no smoke was generated and the film could be stably molded.
  • the film thickness of polyester layer in the obtained release base material was 30 ⁇ m in average.
  • Example 1 An attempt was made to coat the same polyester (B1) as in Example 1 was attempted to coat on a slick paper by using the same laminator as in Example 1 at 145°C . In this coating process, there was little smoke generated and the obtained film was stable. However, when However, when the molding speed was elevated cracking occurred at the selvage of the film. Accordingly, in this case, the lower limit of the thickness of the obtained film was 60 ⁇ m. On the other hand, in evaluating heat resistance of the laminate, the degree of change in the surface gloss depending on temperature was slight, and this was an sufficient result in this respect. However, the close-adhesiveness between the film and the paper was bad and interfacial peeling occurred. Therefore, the obtained product was undesirable as a release base material of the present invention.
  • the release base material was not evaluated for heat resistance, close-adhesiveness, biodegradability, and the like.
  • a 700 L reactor was purged with nitrogen, then 183 kg of 1,4-butanediol and 224 kg of succinic acid were charged in it. After the temperature was elevated under nitrogen stream, esterification by dehydration condensation was carried out for 3.5 hr at 192-220°C , and after ceasing nitrogen charge, for further 3.5 hr under reduced pressures of 20-2 mmHg.
  • a sample collected had an acid value of 9.2 mg/g, a number-average molecular weight (Mn) of 5,160 and a weight average molecular weight (Mw) of 10,670. Subsequently, 34 g of tetraisopropoxy titanium, a catalyst, was added at normal pressures under nitrogen stream.
  • the temperature was elevated to carry out a deglycol-reaction at temperatures of 215-220°C under reduced pressures of 15-0.2 mmHg for 5.5 hr.
  • a sample collected had a number-average molecular weight (Mn) of 16,800 and a weight average molecular weight (Mw) of 43,600.
  • the yield of resulting polyester prepolymer (A2) was 339 kg except condensate water.
  • the obtained polyester (B2) was a slightly ivorylike white, waxy crystal, and had a melting point of 110°C , a number-average molecular weight (Mn) of 35,500 a weight-average molecular weight (Mw) of 170,000, a MFR (190°C ) of 1.0 g/10 min, a viscosity of 230 poises in a 10% ortho-chlorophenol solution and a melt viscosity of 1.5 ⁇ 10 4 poises at a temperature of 190°C at a shear rate of 100 sec -1 .
  • the average molecular weight was measured as in Example 1.
  • the polyester (B2) was extrusion-laminated on a slick paper (70 g/m 2 ) by using of the laminator of Example 1 at 230°C at a line speed of 100 m/min to obtain a release base material having a thickness of 30 ⁇ m.
  • the obtained release base material showed sufficient heat resistance and strong close-adhesiveness to the paper, and cohesive failure of the paper was observed in the peeling test.
  • its biodegradability was evaluated in the same manner as Example 1, after three months, it was observed that there were appeared numerous little holes on the polyester film and the film had partially disappeared. From these results, it was confirmed that decomposition of the film had processed highly.
  • a film comprised of a low density polyester having a thickness of 20 ⁇ m was also evaluated for biodegradability in the earth in the same manner as Example 1.
  • a film comprised of a low density polyester having a thickness of 20 ⁇ m was also evaluated for biodegradability in the earth in the same manner as Example 1.
  • there was no change recognized in appearance and weight and little change in tensile strength and breaking extension of the polyethylene film, and therefore, decomposition had not proceeded.
  • a 700 L reactor was purged with nitrogen, then 177 kg of 1,4-butanediol, 198 kg of succinic acid and 25 kg of adipic acid were charged in it. After the temperature was elevated under nitrogen stream, esterification by dehydration condensation was performed for 3.5 hr at 190-210°C , and after ceasing nitrogen charge, for further 3.5 hr under reduced pressures of 20-2 mmHg.
  • a sample collected had an acid value of 9.6 mg/g, a number-average molecular weight (Mn) of 6,100 and weight-average molecular weight (Mw) of 12,200. Subsequently, 20 g of tetraisopropoxy titanium, a catalyst, was added at normal pressures under nitrogen stream.
  • the temperature was elevated to perform a deglycol-reaction at temperatures of 210-220°C under reduced pressures of 15-0.2 mmHg for 6.5 hr.
  • a sample collected had a number-average molecular weight (Mn) of 17,300 and a weight-average molecular weight (Mw) of 46,400.
  • the resulting polyester (A3) had a yield of 337 kg except condensate water.
  • the obtained polyester (B3) was a slightly ivory-like white, waxy crystal, and had a melting point of 103°C , a number-average molecular weight (Mn) of 36,000, a weight-average molecular weight (Mw) of 200,900, a MFR (190°C ) of 0.52 g/10 min, a viscosity of 680 poises in a 10% orthochlorophenol solution and a melt viscosity of 2.2 ⁇ 10 4 poises at a temperature of 190°C at a shear rate of 100 sec -1 .
  • the polyester (B3) was extrusion-laminated on a slick paper (70 g/m 2 ) at 270°C at a line speed of 150 m/min. In the molding process, although the selvage of the film became somewhat thick, the film width and thickness were stable and, therefore, it was possible to mold the film stably.
  • a 70 L reactor was purged with nitrogen, then 20.0 kg of 1,4-butanediol, 25.0 kg of succinic acid and 284 g of trimethylol propane were charged in it. After the temperature was elevated under nitrogen stream, esterification by dehydration condensation was performed for 3.5 hr at 192-220°C , and after ceasing nitrogen charge, for further 2.5 hr under reduced pressures of 20-2 mmHg.
  • a sample collected had an acid value of 2.5 mg/g, a number-average molecular weight (Mn) of 8.660 and a weight average molecular weight (Mw) of 9,520. Subsequently, 3.7 g of tetraisopropoxy titanium, a catalyst, was added at normal pressures under nitrogen stream.
  • the temperature was elevated to perform a deglycol-reaction at temperatures of 210-220°C under reduced pressures of 15-0.3 mmHg for 8 hr.
  • the resulting polyester (A4) had a yield of 36.7 kg except condensate water.
  • the average molecular weight was measured in the same manner as in Example 1.
  • the selvage of the thin film was stable and there was little generation of smoke in the molding process. In this manner, the release base material could could be stably molded.
  • the obtained release base material had sufficient close-adhesiveness between paper and polyester, and cohesive failure of the paper was observed in the peeling test with no interfacial peeling.
  • the release base material was cut into a 10 cm ⁇ 20 cm of rectangular pieces and they were mounted on square frames made of stainless steel with the pieces held between polyethylene nets. The obtained test pieces were then buried in the earth at a depth of 10 cm to evaluate biodegradability.
  • the test site was the grounds of Kawasaki Plastics Laboratory, SHOWA DENKO K.K. (Kawasaki-ku, Kawasaki-shi). After three months, the test pieces were dug up from the earth. The polyester thin films were more decomposed than paper fibers and had crumbled into decay.
  • the film thickness of polyester layer in the obtained release base material was 25 ⁇ m in average.
  • Example 1 to 6 and Comparative Example 1 to 2 following tests were carried out.
  • the heat resistance was judged on the basis of the changing degree of gloss and the number of pinholes after the film was left in a circulating air oven at 100°C or 110°C for two minutes.
  • Pinholes The number of pinholes was counted after painting the surface with a colored alcohol.
  • the firm-adhesive properties were judged by observation of the behavior of the laminated film upon tearing up the processed laminate paper by hand followed by peeling off its laminated film.
  • the melt film was stable and the stability of the molded film was excellent. Furthermore, there was little generated smoke and the condition of the working environment was good.
  • the release base material was cut into 10 cm x 20 cm rectangular pieces and they were mounted on square frames made of stainless steel with the pieces held between polyethylene nets. The obtained test pieces were then buried in the earth at a depth of 10 cm to evaluate biodegradability.
  • the test site was the grounds of Kawasaki Plastics Laboratory, SHOWA DENKO K.K. (Kawasaki-ku, Kawasaki-shi). After three months, the test pieces were dug up from the earth. The polyester thin films were more decomposed than paper fibers and had crumbled into decay.
  • the aliphatic polyester resin (B1) was extruded and laminated 20 ⁇ m thick on a base paper supplied at a speed of 100 m/min in the same manner as Example 7 at a resin temperature of 190°C to obtain a base material for a paper container.
  • the melt film was stable and the stability of molded film was excellent. Furthermore, there was little smoke and the condition of the working environment was good.
  • the aliphatic polyester resin (B1) was extruded and laminated 60 ⁇ m thick on plate paper supplied at a speed of 50 m/min in the same manner as Example 7 at a resin temperature of 145°C to obtain a base material for a paper containers.
  • the melt viscosity was too high, it was difficult to make a thin polyester resin layer.
  • the lower limit of thickness of the polyester resin layer was 60 ⁇ m and it could not be made any thinner. In the lamination-molding process, the melt film was stable and there was little generated smoke.
  • the aliphatic polyester resin (B2) used in Example 3 was extruded 30 ⁇ m thick on a base paper supplied at a speed of 100 m/min in the same manner as Example 7 at a resin temperature of 230°C to obtain a base material for a paper-made container.
  • the molded film was stable and, furthermore, there was a little generated smoke and the condition of the working environment was good.
  • the aliphatic polyester resin (B2) used in Example 3 was extruded in 20 ⁇ m thick on a base paper supplied at a speed of 100 m/min in a same manner as Example 1 at a resin temperature of 270°C to obtain a base material for a paper container.
  • the neck-in was somewhat large, the evaluation was ⁇ and the molded film was stable.
  • the deterioration level of the working environment was not serious.
  • the neck-in was small and the evaluation was ⁇ , and therefore, the stability of the molded film was very good.
  • the working environment was not seriously deteriorated.
  • the melt film was stable and the stability of the molded film was excellent. Furthermore, there was little generated smoke and the condition of the working environment was good.
  • the release base material was cut into 10 cm ⁇ 20 cm rectangular pieces and they were mounted on square frames made of stainless steel with the pieces held between polyethylene nets. The obtained test pieces were then buried in the earth at a depth of 10 cm to evaluate biodegradability.
  • the test site was the grounds of Kawasaki Plastic Laboratory, SHOWA DENKO K.K. (Kawasaki-ku, Kawasaki-shi). After three months, the test pieces were dug up from the earth. The polyester thin films were more decomposed than paper fibers and had crumbled into decay.
  • the aliphatic polyester resin (B4) used in Example 5 was extruded 30 ⁇ m thick on a base paper supplied at a speed of 100 m/min in the same manner as Example 7 at a resin temperature of 190°C to obtain a base material for a paper-made container.
  • the molded film was stable and, furthermore, there was a little generated smoke and the condition of the working environment was good.
  • the polyester (B1) and the polyester (B4) having long chain branch were blended (1 : 1) and pelletized by an extruder (50 mm ⁇ ) to make a polyester (C1).
  • the polyester (C1) was laminated on a base paper fed at 180 m/min, at resin temperature of 210 °C and 20 ⁇ m thick as the same manner as in Example 7, to make base material for paper container. Smoking was observed few without polluting a working environment.
  • the laminated material was tested for biodegradability as the same manner as in Example 7.
  • the test site was the grounds of Kawasaki Plastic Laboratory, SHOWA DENKO K.K. (Kawasaki-ku, Kawasaki-shi). After three months, the test pieces were dug up from the earth. The polyester thin films were more decomposed than paper fibers and had crumbled into decay.
  • Example 7 - 13 and Comparative Example 3 - 5 were carried out as follows. The results are shown in Table 2.

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EP93302979A 1992-05-08 1993-04-19 Polyester laminates Expired - Lifetime EP0569150B1 (en)

Applications Claiming Priority (62)

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JP116240/92 1992-05-08
JP11623992 1992-05-08
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JP4117653A JP2851478B2 (ja) 1992-05-11 1992-05-11 ポリエステル製モノフィラメント
JP117655/92 1992-05-11
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JP11765792A JP3153621B2 (ja) 1992-05-11 1992-05-11 複合繊維
JP4117655A JP2709235B2 (ja) 1992-05-11 1992-05-11 ポリエステル製捲縮繊維
JP11765892 1992-05-11
JP4117654A JP2709234B2 (ja) 1992-05-11 1992-05-11 ポリエステル製ステープル
JP4117656A JP2709236B2 (ja) 1992-05-11 1992-05-11 ポリエステル製マルチフィラメント
JP117657/92 1992-05-11
JP117654/92 1992-05-11
JP117653/92 1992-05-11
JP119199/92 1992-05-12
JP11919992 1992-05-12
JP119198/92 1992-05-12
JP119195/92 1992-05-12
JP119197/92 1992-05-12
JP11919892 1992-05-12
JP119196/92 1992-05-12
JP11919692 1992-05-12
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JP11919792A JP3238466B2 (ja) 1992-05-12 1992-05-12 ポリエステル製並び繊維
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EP0569150A2 EP0569150A2 (en) 1993-11-10
EP0569150A3 EP0569150A3 (index.php) 1994-01-05
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EP93302979A Expired - Lifetime EP0569150B1 (en) 1992-05-08 1993-04-19 Polyester laminates
EP93302981A Expired - Lifetime EP0569152B1 (en) 1992-05-08 1993-04-19 Non-woven polyester fabric
EP93302980A Expired - Lifetime EP0569151B1 (en) 1992-05-08 1993-04-19 Polyester foamed thin materials
EP93302971A Expired - Lifetime EP0569143B1 (en) 1992-05-08 1993-04-19 Polyester tying tape-like materials
EP93302975A Expired - Lifetime EP0569147B1 (en) 1992-05-08 1993-04-19 Polyester sheet
EP93302977A Expired - Lifetime EP0569149B1 (en) 1992-05-08 1993-04-19 Polyester injection-molded articles
EP93302972A Expired - Lifetime EP0569144B1 (en) 1992-05-08 1993-04-19 Polyester flat and split yarn
EP93302973A Expired - Lifetime EP0569145B1 (en) 1992-05-08 1993-04-19 Polyester fibers
EP97203105A Expired - Lifetime EP0825221B1 (en) 1992-05-08 1993-04-19 Polyester sheet
EP93302982A Expired - Lifetime EP0569153B1 (en) 1992-05-08 1993-04-19 Polyester resin composition
EP93302978A Expired - Lifetime EP0581410B1 (en) 1992-05-08 1993-04-19 Polyester blow-molded articles
EP93303000A Expired - Lifetime EP0569154B1 (en) 1992-05-08 1993-04-19 Biodegradable disposable diaper
EP93302976A Expired - Lifetime EP0569148B1 (en) 1992-05-08 1993-04-19 Polyester foamed articles and method for producing the same
EP93302974A Expired - Lifetime EP0569146B1 (en) 1992-05-08 1993-04-19 Polyester film

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EP93302981A Expired - Lifetime EP0569152B1 (en) 1992-05-08 1993-04-19 Non-woven polyester fabric
EP93302980A Expired - Lifetime EP0569151B1 (en) 1992-05-08 1993-04-19 Polyester foamed thin materials
EP93302971A Expired - Lifetime EP0569143B1 (en) 1992-05-08 1993-04-19 Polyester tying tape-like materials
EP93302975A Expired - Lifetime EP0569147B1 (en) 1992-05-08 1993-04-19 Polyester sheet
EP93302977A Expired - Lifetime EP0569149B1 (en) 1992-05-08 1993-04-19 Polyester injection-molded articles
EP93302972A Expired - Lifetime EP0569144B1 (en) 1992-05-08 1993-04-19 Polyester flat and split yarn
EP93302973A Expired - Lifetime EP0569145B1 (en) 1992-05-08 1993-04-19 Polyester fibers
EP97203105A Expired - Lifetime EP0825221B1 (en) 1992-05-08 1993-04-19 Polyester sheet
EP93302982A Expired - Lifetime EP0569153B1 (en) 1992-05-08 1993-04-19 Polyester resin composition
EP93302978A Expired - Lifetime EP0581410B1 (en) 1992-05-08 1993-04-19 Polyester blow-molded articles
EP93303000A Expired - Lifetime EP0569154B1 (en) 1992-05-08 1993-04-19 Biodegradable disposable diaper
EP93302976A Expired - Lifetime EP0569148B1 (en) 1992-05-08 1993-04-19 Polyester foamed articles and method for producing the same
EP93302974A Expired - Lifetime EP0569146B1 (en) 1992-05-08 1993-04-19 Polyester film

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Families Citing this family (73)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0569150B1 (en) * 1992-05-08 1998-01-07 Showa Highpolymer Co., Ltd. Polyester laminates
DE4329310A1 (de) * 1993-08-31 1995-03-02 Brueggemann L Kg Verfahren zur Herstellung modifizierter Polyester-Formmassen
KR0120829B1 (ko) * 1993-11-03 1997-10-22 박홍기 지방족 공중합 폴리에스터를 이용한 필름의 제조방법
JPH07179736A (ja) * 1993-12-24 1995-07-18 Kanegafuchi Chem Ind Co Ltd 高溶融粘弾性発現性樹脂組成物およびそれを用いた芳香族ポリエステル系樹脂発泡体の製造法
JP2970997B2 (ja) * 1994-07-01 1999-11-02 株式会社クラレ ポリウレタン層を有する積層体
JPH10505620A (ja) * 1994-09-09 1998-06-02 ヒュールス アーゲー 生物学的に分解可能なポリエステルおよび該ポリエステルからなる材料
FR2725731B1 (fr) * 1994-10-12 1996-12-13 Fiberweb Sodoca Sarl Procede de fabrication d'un non-tisse a base d'acide lactique et non-tisse obtenu
DE4437792A1 (de) * 1994-10-21 1996-04-25 Inventa Ag Formmassen auf der Basis von aliphatischen Polyestern
JP2688330B2 (ja) * 1994-10-25 1997-12-10 株式会社日本触媒 ポリエステル樹脂組成物
DE4440837A1 (de) * 1994-11-15 1996-05-23 Basf Ag Biologisch abbaubare Polymere, Verfahren zu deren Herstellung sowie deren Verwendung zur Herstellung bioabbaubarer Formkörper
DE4440858A1 (de) * 1994-11-15 1996-05-23 Basf Ag Biologisch abbaubare Polymere, Verfahren zu deren Herstellung sowie deren Verwendung zur Herstellung bioabbaubarer Formkörper
DE4440850A1 (de) * 1994-11-15 1996-05-23 Basf Ag Biologisch abbaubare Polymere, Verfahren zu deren Herstellung sowie deren Verwendung zur Herstellung bioabbaubarer Formkörper
DE4440836A1 (de) * 1994-11-15 1996-05-23 Basf Ag Biologisch abbaubare Polymere, Verfahren zu deren Herstellung sowie deren Verwendung zur Herstellung bioabbaubarer Formkörper
US5759569A (en) * 1995-01-10 1998-06-02 The Procter & Gamble Company Biodegradable articles made from certain trans-polymers and blends thereof with other biodegradable components
US5648412A (en) * 1995-01-30 1997-07-15 The Dow Chemical Company Blow-moldable rigid thermoplastic polyurethane resins
DE59600710D1 (de) * 1995-02-16 1998-11-26 Basf Ag Biologisch abbaubare polymere, verfahren zu deren herstellung sowie deren verwendung zur herstellung bioabbaubarer formkörper
DE19505185A1 (de) * 1995-02-16 1996-10-24 Basf Ag Biologisch abbaubare Polymere, Verfahren zu deren Herstellung sowie deren Verwendung zur Herstellung bioabbaubarer Formkörper
FR2733520B1 (fr) * 1995-04-26 1997-06-06 Fiberweb Sodoca Structure composite biodegradable non tisse/film
FR2735483B1 (fr) * 1995-06-13 1997-08-08 Potency Sarl Materiau composite totalement biodegradable et procede de fabrication de ce materiau
WO1997002375A1 (en) * 1995-06-30 1997-01-23 Kimberly-Clark Worldwide, Inc. Water-degradable multicomponent fibers and nonwovens
US5916678A (en) * 1995-06-30 1999-06-29 Kimberly-Clark Worldwide, Inc. Water-degradable multicomponent fibers and nonwovens
DE19615356A1 (de) * 1996-04-18 1997-10-23 Bayer Ag Kompostierbare und thermoplastisch verarbeitbare Schaumstoffe
US5661193A (en) * 1996-05-10 1997-08-26 Eastman Chemical Company Biodegradable foamable co-polyester compositions
DE19630236A1 (de) * 1996-07-26 1998-01-29 Wolff Walsrode Ag Biaxial gereckte, biologisch abbaubare und kompostierbare Wursthülle
JP3229978B2 (ja) * 1997-05-26 2001-11-19 株式会社ジエイエスピー 脂肪族ポリエステル系樹脂発泡粒子、その成形体並びに該樹脂発泡粒子の製造方法
US6089009A (en) 1997-08-28 2000-07-18 Belmont Textile Machinery Co., Inc. Fluid-jet false-twisting method and product
US5976694A (en) * 1997-10-03 1999-11-02 Kimberly-Clark Worldwide, Inc. Water-sensitive compositions for improved processability
US6268434B1 (en) 1997-10-31 2001-07-31 Kimberly Clark Worldwide, Inc. Biodegradable polylactide nonwovens with improved fluid management properties
US6201068B1 (en) 1997-10-31 2001-03-13 Kimberly-Clark Worldwide, Inc. Biodegradable polylactide nonwovens with improved fluid management properties
US5910545A (en) * 1997-10-31 1999-06-08 Kimberly-Clark Worldwide, Inc. Biodegradable thermoplastic composition
US6544455B1 (en) 1997-12-22 2003-04-08 Kimberly-Clark Worldwide, Inc. Methods for making a biodegradable thermoplastic composition
US6306782B1 (en) 1997-12-22 2001-10-23 Kimberly-Clark Worldwide, Inc. Disposable absorbent product having biodisintegratable nonwovens with improved fluid management properties
US6309988B1 (en) 1997-12-22 2001-10-30 Kimberly-Clark Worldwide, Inc. Biodisintegratable nonwovens with improved fluid management properties
DE19832456A1 (de) * 1998-07-18 2000-01-20 Bayer Ag Biologisch abbaubare Formmassen mit hoher spezifischer Dichte
US6225388B1 (en) 1998-08-31 2001-05-01 Kimberly-Clark Worldwide, Inc. Biodegradable thermoplastic composition with improved wettability
US6197860B1 (en) 1998-08-31 2001-03-06 Kimberly-Clark Worldwide, Inc. Biodegradable nonwovens with improved fluid management properties
US6194483B1 (en) 1998-08-31 2001-02-27 Kimberly-Clark Worldwide, Inc. Disposable articles having biodegradable nonwovens with improved fluid management properties
DE19847909A1 (de) * 1998-10-19 2000-04-20 Basf Ag Verfahren zur Verbesserung der Standzeit von Filamenten, Fasern oder Folien auf der Basis biologisch abbaubarer Polymerer
DE19919357A1 (de) * 1999-04-28 2000-11-02 Buehler Ag Verfahren zur thermischen Behandlung von PET in fester Phase und Vorrichtung zur Durchführung des Verfahrens
EP1183303B1 (de) 1999-05-10 2005-01-12 Basf Aktiengesellschaft Biologisch abbaubare polyesterschaumstoffpartikel
US6630561B2 (en) * 2000-04-24 2003-10-07 Ube Industries, Ltd. Crystalline polyesterpolyol and hot-melt adhesive
DE10027905A1 (de) * 2000-06-06 2001-12-13 Bayer Ag Biologisch abbaubare Formmassen mit sehr guter Fließfähigkeit sowie deren Herstellung und Verwendung
KR20030068162A (ko) * 2000-11-30 2003-08-19 다이셀 가가꾸 고교 가부시끼가이샤 지방족 폴리에스테르 공중합체 및 그 제조방법, 지방족폴리에스테르계 생분해성 수지 성형물, 및 락톤함유 수지
US20020128344A1 (en) * 2000-12-07 2002-09-12 Yuko Fujihira Biodegradable resin material and method for producing the same
US6500897B2 (en) 2000-12-29 2002-12-31 Kimberly-Clark Worldwide, Inc. Modified biodegradable compositions and a reactive-extrusion process to make the same
US7053151B2 (en) 2000-12-29 2006-05-30 Kimberly-Clark Worldwide, Inc. Grafted biodegradable polymer blend compositions
US6579934B1 (en) 2000-12-29 2003-06-17 Kimberly-Clark Worldwide, Inc. Reactive extrusion process for making modifiied biodegradable compositions
US6552124B2 (en) 2000-12-29 2003-04-22 Kimberly-Clark Worldwide, Inc. Method of making a polymer blend composition by reactive extrusion
US6890989B2 (en) 2001-03-12 2005-05-10 Kimberly-Clark Worldwide, Inc. Water-responsive biodegradable polymer compositions and method of making same
WO2003046060A1 (en) 2001-11-29 2003-06-05 Toray Industries, Inc. Crosslinked biodegradable resin continuous foamed sheet and method for production thereof
ITMI20020865A1 (it) * 2002-04-22 2003-10-22 Novamont Spa Poliesteri biodegradabili ottenuti mediante estrusione reattiva
JP5100946B2 (ja) * 2002-09-25 2012-12-19 株式会社クレハ 強延伸脂肪族ポリエステル重合体成形物
JP3889376B2 (ja) * 2003-05-16 2007-03-07 松下電器産業株式会社 電池用パッケージおよびその製造方法
US8080191B2 (en) 2006-10-20 2011-12-20 Pepsico, Inc. Extrudable polyethylene terephthalate blend
WO2008104541A1 (de) * 2007-02-28 2008-09-04 Basf Se Verfahren zur herstellung von polyesteralkoholen
BE1018018A6 (nl) 2008-02-28 2010-04-06 Gielen Cornelis Oplossing voor het biologisch reinigen van tandenborstels en bijhorende inrichting.
CN101977963B (zh) * 2008-03-28 2013-03-27 三菱化学株式会社 脂肪族聚酯的制造方法
TR201904238T4 (tr) 2008-04-18 2019-04-22 Pepsico Inc Ekstrüzyon üflemeli kalıplama ile ürünlerin hazırlanmasına yönelik polyester bileşimleri ve yöntem.
US8858986B2 (en) 2008-06-12 2014-10-14 3M Innovative Properties Company Biocompatible hydrophilic compositions
MX345585B (es) * 2008-06-12 2017-02-07 3M Innovative Properties Co Fibras finas hiladas por fusion mediante soplado y metodos de manufactura.
AU2013263831B2 (en) * 2008-06-12 2016-07-07 3M Innovative Properties Company Melt blown fine fibers and methods of manufacture
US9487893B2 (en) 2009-03-31 2016-11-08 3M Innovative Properties Company Dimensionally stable nonwoven fibrous webs and methods of making and using the same
CA2779361A1 (en) * 2009-11-09 2011-05-12 Basf Se Method for producing shrink films
EP2513365A4 (en) 2009-12-17 2013-09-18 3M Innovative Properties Co DIMENSION-STABLE FIBER-NETS, MELT-BLOWN FIBER-FIBERS, AND METHOD FOR THEIR PRODUCTION AND USE
MX347302B (es) 2009-12-17 2017-04-21 3M Innovative Properties Company * Telas fibrosas no tejidas dimensionalmente estables y metodos para fabricar y utilizar las mismas.
TW201221714A (en) 2010-10-14 2012-06-01 3M Innovative Properties Co Dimensionally stable nonwoven fibrous webs and methods of making and using the same
US10273356B2 (en) 2013-06-18 2019-04-30 Total Research & Technology Feluy Polymer composition
CN108484866A (zh) * 2018-04-28 2018-09-04 袁杰 一种亲油稳定型聚氨酯泡沫材料的制备方法
CN109810666B (zh) * 2018-12-21 2020-10-30 中山市康和化工有限公司 一种具有降解特性的聚氨酯胶粘剂及其制备方法
CN110305305B (zh) * 2019-07-09 2020-05-15 山东大学 一种医用纤维热熔被覆树脂及其制备方法
WO2024028420A1 (en) 2022-08-05 2024-02-08 Fitesa Germany Gmbh Nonwoven fabric and process for forming the same
WO2025098944A1 (en) 2023-11-10 2025-05-15 Fitesa Germany Gmbh Nonwoven fabric and process for forming the same
WO2025098942A1 (en) 2023-11-10 2025-05-15 Fitesa Germany Gmbh Nonwoven fabric and process for forming the same

Family Cites Families (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE440217A (fr) * 1940-01-17 1941-02-28 Ig Farbenindustrie Ag Procédé pour la production de polyesters contenant des groupes amides à poids moléculaire élevé
BE529733A (index.php) * 1953-06-19
US3524825A (en) * 1957-05-29 1970-08-18 Gen Motors Corp Polyurethane foam and method for making same
US2999851A (en) * 1957-12-16 1961-09-12 Gen Tire & Rubber Co Isocyanate extension of very high molecular weight polyesters
BE574488A (index.php) * 1958-01-09
NL251761A (index.php) * 1960-03-17 1900-01-01
CH501025A (de) * 1968-12-17 1970-12-31 Ciba Geigy Ag In hochmolekulare, kristalline Polyurethan-Kunststoffprodukte umwandelbare Formmassen auf Basis von Diisocyanaten und schwach verzweigten Polyestern
FR2233166B1 (index.php) * 1972-10-25 1976-10-29 Rhone Poulenc Ind
US4057537A (en) * 1975-01-28 1977-11-08 Gulf Oil Corporation Copolymers of L-(-)-lactide and epsilon caprolactone
US4031065A (en) * 1975-03-06 1977-06-21 Basf Aktiengesellschaft Manufacture of thermoplastic polyester molding compositions of high viscosity
US4076798A (en) * 1975-05-29 1978-02-28 American Cyanamid Company High molecular weight polyester resin, the method of making the same and the use thereof as a pharmaceutical composition
GB1518500A (en) * 1975-10-24 1978-07-19 Courtaulds Ltd Bicomponent filaments
CA1096536A (en) * 1976-03-22 1981-02-24 John R. Costanza Polymers for extrusion applications
GB2021602B (en) * 1978-05-24 1982-10-20 Ici Ltd Polymeric materials
DE3028501A1 (de) * 1980-07-26 1982-03-04 Basf Ag, 6700 Ludwigshafen Thermoplastisch verarbeitbare polyurethan-elastomere mit verbesserter abriebbestaendigkeit und ein verfahren zu deren herstellung
US4442282A (en) * 1983-06-20 1984-04-10 The B. F. Goodrich Company Polyurethane covered golf balls
JPS6433201A (en) * 1987-07-29 1989-02-03 Dainippon Ink & Chemicals Thermoplastic elastic tape for paper diaper
GB8728358D0 (en) * 1987-12-04 1988-01-13 Bostik Ltd Sheet materials
DE3810595A1 (de) * 1988-03-29 1989-10-12 Wolff Walsrode Ag Thermoplastische folien
JPH02106323A (ja) * 1988-10-14 1990-04-18 Mitsubishi Heavy Ind Ltd 形状記憶性透明体及びその成形法
CA2015488C (en) * 1989-04-30 1997-07-08 Tomoyasu Tsuda Polyurethane, process for its production and polyester diol used for its production
US5026589A (en) * 1989-12-28 1991-06-25 The Procter & Gamble Company Disposable sanitary articles
GB2243327A (en) * 1990-02-16 1991-10-30 Procter & Gamble Biodegradable, liquid-impervious sheet laminate
DE4006648A1 (de) * 1990-03-03 1991-09-05 Basf Ag Verfahren zur herstellung von zellhaltigen polyurethan-formkoerpern durch sinterung
GB9006589D0 (en) * 1990-03-23 1990-05-23 Bostik Ltd Improved reinforcing material
US5053482A (en) * 1990-05-11 1991-10-01 E. I. Du Pont De Nemours And Company Novel polyesters and their use in compostable products such as disposable diapers
DE4015714A1 (de) * 1990-05-16 1991-11-21 Bayer Ag Thermoplastische pu-schaeume mit glasfaserverstaerkung
US5037410A (en) * 1990-08-08 1991-08-06 Zimmerman Robert R Disposable articles comprising compostible components
US5306787A (en) * 1990-11-26 1994-04-26 Showa Highpolymer Co., Ltd. Method for producing saturated polyester
DE4119455C1 (index.php) * 1991-06-13 1992-09-17 Fa. Carl Freudenberg, 6940 Weinheim, De
AU668356B2 (en) * 1991-06-26 1996-05-02 Procter & Gamble Company, The Disposable absorbent articles with biodegradable backsheets
JP2860183B2 (ja) * 1991-08-06 1999-02-24 昭和高分子株式会社 ウレタン結合を含むポリエステルの製造方法
JP2860185B2 (ja) * 1991-08-06 1999-02-24 昭和高分子株式会社 ウレタン結合を含むポリエステルの製造方法
JP3046657B2 (ja) * 1991-09-10 2000-05-29 昭和高分子株式会社 ウレタン結合を含む脂肪族ポリエステルの製造方法
JP3046659B2 (ja) * 1991-09-10 2000-05-29 昭和高分子株式会社 ウレタン結合を含む脂肪族ポリエステルの製造方法
JP3354164B2 (ja) * 1991-09-10 2002-12-09 昭和高分子株式会社 脂肪族ポリエステル組成物
WO1993013152A1 (fr) * 1991-12-20 1993-07-08 Showa Highpolymer Co., Ltd. Procede d'elaboration d'un polyester aliphatique a forte structure moleculaire et film realise a partir de ce polyester
JP3179177B2 (ja) * 1992-04-10 2001-06-25 昭和高分子株式会社 ウレタン結合を含む脂肪族ポリエステル
EP0569150B1 (en) * 1992-05-08 1998-01-07 Showa Highpolymer Co., Ltd. Polyester laminates

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EP0569145A3 (en) 1993-12-08
EP0569144B1 (en) 1997-11-19
EP0569152A3 (index.php) 1994-01-05
EP0825221A1 (en) 1998-02-25
EP0569153A2 (en) 1993-11-10
EP0569149A2 (en) 1993-11-10
EP0569146A3 (en) 1993-12-08
EP0569154A1 (en) 1993-11-10
EP0569147A3 (en) 1993-12-08
EP0569153A3 (index.php) 1994-01-05
EP0569145A2 (en) 1993-11-10
EP0569152A2 (en) 1993-11-10
EP0569147A2 (en) 1993-11-10
EP0569143B1 (en) 1998-03-18
EP0569151B1 (en) 1998-03-25
EP0825221B1 (en) 2001-07-11
EP0569154B1 (en) 2000-01-05
EP0569153B1 (en) 1999-10-06
EP0569148A1 (en) 1993-11-10
EP0569148B1 (en) 1998-02-04
EP0569150A2 (en) 1993-11-10
EP0569143A3 (en) 1994-01-05
EP0581410A1 (en) 1994-02-02
EP0569144A3 (en) 1993-12-01
EP0569146A2 (en) 1993-11-10
EP0569143A2 (en) 1993-11-10
EP0569149A3 (en) 1993-12-01
EP0581410B1 (en) 1997-10-22
EP0569147B1 (en) 1999-11-17
EP0569144A2 (en) 1993-11-10
EP0569149B1 (en) 1998-07-15
EP0569152B1 (en) 1998-10-14
EP0569145B1 (en) 1999-03-24
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EP0569146B1 (en) 2000-02-09

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